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(1) R_v = \exp \big [ 3.684 + 0.61967 \cdot Z + 0.015359 \cdot Z^2 \big ]
(2) Z = \sum_{n=1}^4 \, Z_n
(3) Z_n = C_{n0} + C_{n1} \cdot {\rm VAR}_n + C_{n2} \cdot {\rm VAR}_n^2 + C_{n3} \cdot {\rm VAR}_n^3 + C_{n4} \cdot {\rm VAR}_n^4

where

R_v

stb/MMscf Vaporized Oil Ratio

and

nVARn

Cn0Cn1Cn2Cn3Cn4
1

\ln p

Fluid pressurepsia20.809-6.70950.513600
2

\gamma_{o{\rm API}}

Initial stock-tank condensate API gravity

°API11.175-1.29650.042311-0.00054382.49E-6
3

\gamma_{g Rd}

Gas specific gravity recombined to the dew pointfrac-13.36527.652-18.5984.36580
4

T_r

Fluid  temperature°F-1.53090.00584531.4E-600


The correlation is built over the following range:




MinimumMeanMaximum
Vaporized Oil Ratio at separator

R_v

stb/MMscf8.3451.55247.46
Vaporized Oil Ratio for recombined dewpoint gas composition

R_{vd}

stb/MMscf17.95144.66417.60
Initial stock-tank condensate API gravity for recombined dewpoint gas composition

\gamma_{o{\rm API}}

°API37.853.876.5
Gas specific gravity for recombined dewpoint gas composition

\gamma_{g Rd}

frac0.6431.0441.568
Fluid  temperature

T

°F126247.1348
Fluid pressure

p

psia1,114.73,083.39,014.7


The correlation has been built for the R_v measured at the first stage of separator (as the oil yield measurements at second stage separator and stock tank are not readily available).

This means that further corrections may be required to get accurate values of R_v in respect to STP.

See also


Natural Science / Physics /Thermodynamics / Equation of State / Vaporized Oil Ratio (Rv)

References


Ovalle, Adriana P., Lenn, Christopher Peter, and William D. McCain. "Tools To Manage Gas/Condensate Reservoirs; Novel Fluid-Property Correlations on the Basis of Commonly Available Field Data." SPE Res Eval & Eng 10 (2007): 687–694. doi.org/10.2118/112977-PA




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